WO2009032959A2 - Procédés de fabrication de dialkyl éthers à partir d'alcools - Google Patents

Procédés de fabrication de dialkyl éthers à partir d'alcools Download PDF

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WO2009032959A2
WO2009032959A2 PCT/US2008/075302 US2008075302W WO2009032959A2 WO 2009032959 A2 WO2009032959 A2 WO 2009032959A2 US 2008075302 W US2008075302 W US 2008075302W WO 2009032959 A2 WO2009032959 A2 WO 2009032959A2
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group
degrees
methylimidazolium
straight
ionic liquid
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PCT/US2008/075302
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WO2009032959A3 (fr
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Mark Andrew Harmer
Michael B. D'amore
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E. I. Du Pont De Nemours And Company
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Priority to EP08829069A priority Critical patent/EP2185495A2/fr
Priority to JP2010524155A priority patent/JP2010538082A/ja
Priority to US12/676,160 priority patent/US20100197974A1/en
Priority to CN200880105427.0A priority patent/CN101796010A/zh
Publication of WO2009032959A2 publication Critical patent/WO2009032959A2/fr
Publication of WO2009032959A3 publication Critical patent/WO2009032959A3/fr

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    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C41/00—Preparation of ethers; Preparation of compounds having groups, groups or groups
    • C07C41/01—Preparation of ethers
    • C07C41/09—Preparation of ethers by dehydration of compounds containing hydroxy groups

Definitions

  • This invention is concerned with processes for the preparation of dialkyl ethers from straight-chain alcohols.
  • Ethers such as dibutyl ether are useful as solvents and as diesel fuel cetane enhancers. See, for example, Kotrba, "Ahead of the Curve", Ethanol Producer Magazine, November 2005; and WO 01/18154, wherein an example of a diesel fuel formulation comprising dibutyl ether is disclosed.
  • ethers from alcohol such as the production of dibutyl ether from butanol
  • the reaction is generally carried out via the dehydration of an alcohol by sulfuric acid, or by catalytic dehydration over ferric chloride, copper sulfate, silica, or silica- alumina at high temperatures.
  • Bringue et al J. Catalysis (2006) 244:33-42] disclose thermally stable ion-exchange resins for use as catalysts for the dehydration of 1-pentanol to di-n-pentyl ether.
  • WO 07/38360 discloses a method for making polytrimethylene ether glycols in the presence of an ionic liquid.
  • the inventions disclosed herein include processes for the preparation of dialkyl ethers from alcohols, the use of such processes, and the products obtained and obtainable by such processes.
  • a dialkyl ether is prepared in a reaction mixture by (a) contacting at least one C 4 to Cs straight-chain alcohol with at least one homogeneous acid catalyst in the presence of at least one ionic liquid to form (i) a dialkyl ether phase of the reaction mixture that comprises a dialkyl ether, and (ii) an ionic liquid phase of the reaction mixture; and (b) separating the dialkyl ether phase of the reaction mixture from the ionic liquid phase of the reaction mixture to recover a dialkyl ether product; wherein an ionic liquid is represented by the structure of the Formula Z + A " as set forth below.
  • Ethers such as the dialkyl ethers produced by the processes hereof, are useful as solvents, plasticizers and as additives in transportation fuels such as gasoline, diesel fuel and jet fuel.
  • Figure 1 shows vials in which dibutyl ether is formed from 1-butanol.
  • the vial on the left contains 1-butanol, a homogeneous acid catalyst and an ionic liquid.
  • the vial on the right (labeled “Products”) contains, above the line indicated by the arrow, a phase (labeled "Dibutyl ether”) in which the dibutyl ether product resides, and contains below the line a phase (labeled "IL/acid”) in which an ionic liquid and an acid catalyst or catalyst residue reside .
  • alkane or “alkane compound” is a saturated hydrocarbon having the general formula C n H2n + 2, and may be a straight-chain, branched or cyclic compound.
  • alkene or “alkene compound” is an unsaturated hydrocarbon that contains one or more carbon-carbon double bonds, and may be a straight-chain, branched or cyclic compound.
  • alkoxy radical is a straight-chain or branched alkyl group bound via an oxygen atom.
  • alkyl radical is a univalent group derived from an alkane by removing a hydrogen atom from any carbon atom:
  • the alkyl radical may be a Ci ⁇ C20 straight-chain, branched or cycloalkyl radical.
  • suitable alkyl radicals include methyl, ethyl, n-propyl, i-propyl, n-butyl, t-butyl, n-pentyl, n-hexyl, cyclohexyl, n-octyl, trimethylpentyl, and cyclooctyl radicals.
  • aromatic or “aromatic compound” includes benzene and compounds that resemble benzene in chemical behavior .
  • aryl radical is a univalent group whose free valence is to a carbon atom of an aromatic ring.
  • the aryl moiety may contain one or more aromatic rings and may be substituted by inert groups, i.e. groups whose presence does not interfere with the reaction.
  • suitable aryl groups include phenyl, methylphenyl, ethylphenyl, n-propylphenyl, n- butylphenyl, t-butylphenyl, biphenyl, naphthyl and ethylnaphthyl radicals.
  • a "fluoroalkoxy" radical is an alkoxy radical in which at least one hydrogen atom is replaced by a fluorine atom.
  • a "fluoroalkyl” radical is an alkyl radical in which at least one hydrogen atom is replaced by a fluorine atom.
  • halogen is a bromine, iodine, chlorine or fluorine atom.
  • a “heteroalkyl” radical is an alkyl group having one or more heteroatoms .
  • a “heteroaryl” radical is an aryl group having one or more heteroatoms .
  • a "heteroatom” is an atom other than carbon in the structure of a radical.
  • Optionally substituted with at least one member selected from the group consisting of when referring to an alkane, alkene, alkoxy, alkyl, aryl, fluoroalkoxy, fluoroalkyl, heteroalkyl, heteroaryl, perfluoroalkoxy, or perfluoroalkyl radical or moiety, means that one or more hydrogens on a carbon chain of the radical or moiety may be independently substituted with one or more of the members of a recited group of substituents .
  • an optionally substituted - C2H5 radical or moiety may, without limitation, be - CF 2 CF 3 , -CH 2 CH 2 OH or -CF 2 CF 2 I where the group of substituents consist of F, I and OH.
  • a "perfluoroalkoxy" radical is an alkoxy radical in which all hydrogen atoms are replaced by fluorine atoms .
  • a "perfluoroalkyl” radical is an alkyl radical in which all hydrogen atoms are replaced by fluorine atoms .
  • a dialkyl ether is prepared in a reaction mixture by (a) contacting at least one C 4 to Cs straight-chain alcohol with at least one homogeneous acid catalyst in the presence of at least one ionic liquid to form (i) a dialkyl ether phase of the reaction mixture that comprises a dialkyl ether, and (ii) an ionic liquid phase of the reaction mixture; and (b) separating the dialkyl ether phase of the reaction mixture from the ionic liquid phase of the reaction mixture to recover a dialkyl ether product; wherein an ionic liquid is represented by the structure of the Formula Z + A " as set forth below.
  • Suitable alcohols for use herein to prepare a dialkyl ether include straight-chain alcohols such as n-butanol, n-pentanol, n-hexanol, n-heptanol and n- octanol.
  • a dialkyl ether as prepared by a process hereof may thus be a di-n-alkyl ether, but it may also be an ether in which one or both of the carbon chains thereon are derived from the same or different isomers of a C 4 to Cs straight-chain alcohol.
  • one or both butyl moieties of the dialkyl ether product can independently be 1 -butyl, 2-butyl, t-butyl or isobutyl.
  • Z is a cation selected from the group consisting of:
  • R 1 , R 2 , R 3 , R 4 , R 5 and R 6 are independently selected from the group consisting of: (i) H
  • R 7 , R 8 , R 9 , and R 10 are independently selected from the group consisting of:
  • R 1 , R 2 , R 3 , R 4 , R 5 , R 6 ' R 7 , R 8 , R 9 , and R 10 can together form a cyclic or bicyclic alkanyl or alkenyl group; and
  • a " is an anion selected from the group consisting of R ⁇ -SO 3 " and (R 12 -SO 2 ) 2 N ⁇ ; wherein R 11 and R 12 are independently selected from the group consisting of:
  • the anion A " is selected from the group consisting of : [CH 3 OSO 3 ] “ , [C 2 H 5 OSO 3 ] “ , [CF 3 SO 3 ] “ , [HCF 2 CF 2 SO 3 ] “ , [CF 3 HFCCF 2 SO 3 ] “ , [HCCIFCF 2 SO 3 ] “ , [ (CF 3 SOz) 2 N] “ , [ (CF 3 CF 2 SO 2 ) 2 N] " , [CF 3 OCFHCF 2 SO 3 ] " ,
  • an ionic liquid is selected from the group consisting of l-butyl-2,3- dimethylimidazolium 1, 1, 2, 2-tetrafluoroethanesulfonate, 1-butyl-methylimidazolium 1,1,2,2- tetrafluoroethanesulfonate, 1 -ethyl-3-methylimidazolium 1,1,2, 2-tetrafluoroethanesulfonate, l-ethyl-3- methylimidazolium 1,1,2,3,3,3- hexafluoropropanesulfonate, l-hexyl-3-methylimidazolium 1,1,2,2- tetrafluoroethanesulfonate, l-dodecyl-3- methylimidazolium 1,1,2, 2-tetrafluoroethanesulfonate, l-hexadecyl-3-methylimidazolium 1,1,2, 2-tetrafluoroethan
  • Ionic liquids are organic compounds that are liquid at room temperature (approximately 25°C) . They differ from most salts in that they have very low melting points, they tend to be liquid over a wide temperature range, and have been shown to have high heat capacities. Ionic liquids have essentially no vapor pressure, and they can either be neutral, acidic or basic. The properties of an ionic liquid will show some variation according to the identity of the cation and anion. However, a cation or anion of an ionic liquid useful for this invention can in principle be any cation or anion such that the cation and anion together form an organic salt that is fluid at or below about 100 0 C.
  • ionic liquids are formed by reacting a nitrogen-containing heterocyclic ring, preferably a heteroaromatic ring, with an alkylating agent (for example, an alkyl halide) to form a quaternary ammonium salt, and performing ion exchange or other suitable reactions with various Lewis acids or their conjugate bases to form the ionic liquid.
  • alkylating agent for example, an alkyl halide
  • suitable heteroaromatic rings include substituted pyridines, imidazole, substituted imidazole, pyrrole and substituted pyrroles.
  • These rings can be alkylated with virtually any straight, branched or cyclic Ci_ 2 o alkyl group, but preferably, the alkyl groups are Ci_i 6 groups, since groups larger than this may produce low melting solids rather than ionic liquids.
  • Various triarylphosphines, thioethers and cyclic and non-cyclic quaternary ammonium salts may also been used for this purpose.
  • Counterions that may be used include chloroaluminate, bromoaluminate, gallium chloride, tetrafluoroborate, tetrachloroborate, hexafluorophosphate, nitrate, trifluoromethane sulfonate, methylsulfonate, p-toluenesulfonate, hexafluoroantimonate, hexafluoroarsenate, tetrachloroaluminate, tetrabromoaluminate, perchlorate, hydroxide anion, copper dichloride anion, iron trichloride anion, zinc trichloride anion, as well as various lanthanum, potassium, lithium, nickel, cobalt, manganese, and other metal-containing anions.
  • Ionic liquids may also be synthesized by salt metathesis, by an acid-base neutralization reaction or by quaternizing a selected nitrogen-containing compound; or they may be obtained commercially from several companies such as Merck (Darmstadt, Germany) or BASF (Mount Olive, NJ) .
  • a library i.e. a combinatorial library, of ionic liquids may be prepared, for example, by preparing various alkyl derivatives of a quaternary ammonium cation, and varying the associated anions.
  • the acidity of the ionic liquids can be adjusted by varying the molar equivalents and type and combinations of Lewis acids.
  • fluoroalkyl sulfonate anions may be synthesized from perfluorinated terminal olefins or perfluorinated vinyl ethers generally according to the method of Koshar et al [J. Am. Chem. Soc. (1953) 75:4595-4596]; in one embodiment, sulfite and bisulfite are used as the buffer in place of bisulfite and borax, and in another embodiment, the reaction is carried out in the absence of a radical initiator. 1,1,2,2-
  • Preferred modifications include using a mixture of sulfite and bisulfite as the buffer, freeze drying or spray drying to isolate the crude 1,1,2,2- tetrafluoroethanesulfonate and 1,1,2,3,3,3- hexafluoropropanesulfonate products from the aqueous reaction mixture, using acetone to extract the crude 1, 1, 2, 2-tetrafluoroethanesulfonate and 1,1,2,3,3,3- hexafluoropropanesulfonate salts, and crystallizing 1, 1, 2-trifluoro-2- (trifluoromethoxy) ethanesulfonate and 1, 1, 2-trifluoro-2- (pentafluoroethoxy) ethanesulfonate from the reaction mixture by cooling.
  • ionic liquids suitable for use herein may be made as follows: A first solution is made by dissolving a known amount of the halide salt of the cation in deionized water. This may involve heating to ensure total dissolution. A second solution is made by dissolving an aproximately equimolar amount (relative to the cation) of the potassium or sodium salt of the anion in deionized water. This may also involve heating to ensure total dissolution. Although it is not necessary to use equimolar quantities of the cation and anion, a 1:1 equimolar ratio minimizes the impurities obtained by the reaction.
  • the first and second aqueous solutions are mixed and stirred at a temperature that optimizes the separation of the desired product phase as either an oil or a solid on the bottom of the flask.
  • the aqueous solutions are mixed and stirred at room temperature, however the optimal temperature may be higher or lower based on the conditions necessary to achieve optimal product separation.
  • the water layer is separated, and the product is washed several times with deionized water to remove chloride or bromide impurities. An additional base wash may help to remove acidic impurities.
  • the product is then diluted with an appropriate organic solvent (chloroform, methylene chloride, etc.) and dried over anhydrous magnesium sulfate or other preferred drying agent.
  • the appropriate organic solvent is one that is miscible with the ionic liquid and that can be dried.
  • the drying agent is removed by suction filtration and the organic solvent is removed in vacuo. High vacuum is applied for several hours or until residual water is removed.
  • the final product is usually in the form of a liquid.
  • ionic liquids suitable for use herein may be made as follows: A third solution is made by dissolving a known amount of the halide salt of the cation in an appropriate solvent. This may involve heating to ensure total dissolution.
  • the solvent is one in which the cation and anion are miscible, and in which the salts formed by the reaction are minimally miscible; in addition, the appropriate solvent is preferably one that has a relatively low boiling point such that the solvent can be easily removed after the reaction.
  • Appropriate solvents include, but are not limited to, high purity dry acetone, alcohols such as methanol and ethanol, and acetonitrile .
  • a fourth solution is made by dissolving an equimolar amount (relative to the cation) of the salt (generally potassium or sodium) of the anion in an appropriate solvent, typically the same as that used for the cation. This may also involve heating to ensure total dissolution.
  • the third and fourth solutions are mixed and stirred under conditions that result in approximately complete precipitation of the halide salt byproduct (generally potassium halide or sodium halide) ; in one embodiment of the invention, the solutions are mixed and stirred at approximately room temperature for about 4-12 hours.
  • the halide salt is removed by suction filtration through an acetone/celite pad, and color can be reduced through the use of decolorizing carbon as is known to those skilled in the art.
  • the solvent is removed in vacuo and then high vacuum is applied for several hours or until residual water is removed.
  • the final product is usually in the form of a liquid.
  • the physical and chemical properties of ionic liquids will show some variation according to the identity of the cation and/or anion. For example, increasing the chain length of one or more alkyl chains of the cation will affect properties such as the melting point, hydrophilicity/lipophilicity, density and solvation strength of the ionic liquid.
  • Choice of the anion can affect, for example, the melting point, the water solubility and the acidity and coordination properties of the composition. Effects of choice of cation and anion on the physical and chemical properties of ionic liquids are reviewed by Wasserscheid and Keim [Angew. Chem. Int. Ed. (2000) 39:3772-3789] and Sheldon [Chem. Commun . (2001) 2399- 2407] .
  • An ionic liquid may be present in the reaction mixture in an amount of about 0.1% or more, or about 2% or more, and yet in an amount of about 25% or less, or about 20% or less, by weight relative to the weight of the C 4 to Cs alcohol present therein.
  • a catalyst suitable for use in a process hereof is a substance that increases the rate of approach to equilibrium of the reaction without itself being substantially consumed in the reaction.
  • the catalyst is a homogeneous catalyst in the sense that the catalyst and reactants occur in the same phase, which is uniform, and the catalyst is molecularly dispersed with the reactants in that phase.
  • suitable acids for use herein as a homogeneous catalyst are those having a pKa of less than about 4; in another embodiment, suitable acids for use herein as a homogeneous catalyst are those having a pKa of less than about 2.
  • a homogeneous acid catalyst suitable for use herein may be selected from the group consisting of inorganic acids, organic sulfonic acids, heteropolyacids, fluoroalkyl sulfonic acids, metal sulfonates, metal trifluoroacetates, compounds thereof and combinations thereof.
  • the homogeneous acid catalyst may be selected from the group consisting of sulfuric acid, fluorosulfonic acid, phosphorous acid, p-toluenesulfonic acid, benzenesulfonic acid, phosphotungstic acid, phosphomolybdic acid, trifluoromethanesulfonic acid, nonafluorobutanesulfonic acid, 1,1,2,2- tetrafluoroethanesulfonic acid, 1,1,2,3,3,3- hexafluoropropanesulfonic acid, bismuth triflate, yttrium triflate, ytterbium triflate, neodymium triflate, lanthanum triflate, scandium triflate, and zirconium triflate.
  • a catalyst may be present in the reaction mixture in an amount of about 0.1% or more, or about 1% or more, and yet in an amount of about 20% or less, or about 10% or less, or about 5% or less, by weight relative to the weight of the C 4 to C 8 alcohol present therein .
  • the reaction may be carried out at a temperature of from about 50 degrees C to about 300 degrees C. In one embodiment, the temperature is from about 100 degrees C to about 250 degrees C.
  • the reaction may be carried out at a pressure of from about atmospheric pressure (about 0.1 MPa) to about 20.7 MPa. In a more specific embodiment, the pressure is from about 0.1 MPa to about 3.45 MPa.
  • the reaction may be carried out under an inert atmosphere, for which inert gases such as nitrogen, argon and helium are suitable.
  • the reaction is carried out in the liquid phase.
  • the reaction is carried out at an elevated temperature and/or pressure such that the product dialkyl ethers are present in a vapor phase.
  • Such vapor phase dialkyl ethers can be condensed to a liquid by reducing the temperature and/or pressure. The reduction in temperature and/or pressure can occur in the reaction vessel itself, or alternatively the vapor phase can be collected in a separate vessel, where the vapor phase is then condensed to a liquid phase.
  • the time for the reaction will depend on many factors, such as the reactants, reaction conditions and reactor, and may be adjusted to achieve high yields of dialkyl ethers.
  • the reaction can be carried out in batch mode, or in continuous mode.
  • dialkyl ether phase a first phase of the reaction mixture that is separate from a second phase (an "ionic liquid phase") in which the ionic liquid and catalyst reside.
  • ionic liquid phase an “ionic liquid phase” in which the ionic liquid and catalyst reside.
  • the separated ionic liquid phase may be recycled for addition again to the reaction mixture.
  • the conversion of one or more n- alcohols to one or more dialkyl ethers results in the formation of water. Therefore, where it is desired to recycle the ionic liquid contained in the ionic liquid phase, it may be necessary to treat the ionic liquid phase to remove water.
  • One common treatment method for the removal of water is the use of distillation. Ionic liquids have negligible vapor pressure, and the catalysts useful in this invention generally have boiling points above that of water; therefore it is generally possible when distilling the ionic liquid phase to remove water from the top of a distillation column, whereas an ionic liquid and a catalyst would be removed from the bottom of the column.
  • catalyst residue may be separated from an ionic liquid by filtration or centrifugation, or catalyst residue may be returned to the reaction mixture along with the ionic liquid.
  • the separated and/or recovered dialkyl ether phase can optionally be further purified and used as such.
  • an ionic liquid formed by selecting any of the individual cations described or disclosed herein, and by selecting any of the individual anions described or disclosed herein may be used in a reaction mixture to prepare a dialkyl ether.
  • a subgroup of ionic liquids formed by selecting (i) a subgroup of any size of cations, taken from the total group of cations described and disclosed herein in all the various different combinations of the individual members of that total group, and (ii) a subgroup of any size of anions, taken from the total group of anions described and disclosed herein in all the various different combinations of the individual members of that total group, may be used in a reaction mixture to prepare a dialkyl ether.
  • the ionic liquid or subgroup will be used in the absence of the members of the group of cations and/or anions that are omitted from the total group thereof to make the selection, and, if desirable, the selection may thus be made in terms of the members of the total group that are omitted from use rather than the members of the group that are included for use.
  • Each of the formulae shown herein describes each and all of the separate, individual compounds that can be assembled in that formula by (1) selection from within the prescribed range for one of the variable radicals, substituents or numerical coefficents while all of the other variable radicals, substituents or numerical coefficents are held constant, and (2) performing in turn the same selection from within the prescribed range for each of the other variable radicals, substituents or numerical coefficents with the others being held constant.
  • a plurality of compounds may be described by selecting more than one but less than all of the members of the whole group of radicals, substituents or numerical coefficents.
  • substituents or numerical coefficents is a subgroup containing (i) only one of the members of the whole group described by the range, or (ii) more than one but less than all of the members of the whole group, the selected member (s) are selected by omitting those member (s) of the whole group that are not selected to form the subgroup.
  • the compound, or plurality of compounds may in such event be characterized by a definition of one or more of the variable radicals, substituents or numerical coefficents that refers to the whole group of the prescribed range for that variable but where the member (s) omitted to form the subgroup are absent from the whole group.
  • NMR Nuclear magnetic resonance
  • GC gas chromatography
  • GC-MS gas chromatography- mass spectrometry
  • TLC thin layer chromatography
  • thermogravimetric analysis using a Universal V3.9A TA instrument analyser (TA Instruments, Inc., Newcastle, DE) is abbreviated TGA. Centigrade is abbreviated C, mega
  • Pascal is abbreviated MPa
  • gram is abbreviated g
  • kilogram is abbreviated Kg
  • milliliter (s) is abbreviated ml (s)
  • hour is abbreviated hr or h
  • weight percent is abbreviated wt%
  • milliequivalents is abbreviated meq
  • melting point is abbreviated Mp
  • differential scanning calorimetry is abbreviated DSC.
  • l-Butyl-2 3-dimethylimidazolium chloride, 1-hexyl- 3-methylimidazolium chloride, l-dodecyl-3- methylimidazolium chloride, l-hexadecyl-3-methyl imidazolium chloride, l-octadecyl-3-methylimidazolium chloride, imidazole, tetrahydrofuran, iodopropane, acetonitrile, iodoperfluorohexane, toluene, 1-butanol, oleum (20% SO 3 ), sodium sulfite (Na 2 SO 3 , 98%), and acetone were obtained from Acros (Hampton, NH) .
  • Potassium metabisulfite (K 2 S 2 O 5 , 99%) , was obtained from Mallinckrodt Laboratory Chemicals (Phillipsburg, NJ) . Potassium sulfite hydrate (KHSO 3 *xH 2 O, 95%) , sodium bisulfite (NaHSO 3 ) , sodium carbonate, magnesium sulfate, phosphotungstic acid, ethyl ether, 1,1,1,2,2,3,3,4,4,5,5,6, 6-tridecafluoro-8-iodooctane, trioctyl phosphine and l-ethyl-3-methylimidazolium chloride (98%) were obtained from Aldrich (St. Louis, MO) .
  • Sulfuric acid and methylene chloride were obtained from EMD Chemicals, Inc. (Gibbstown, NJ) .
  • Perfluoro (ethylvinyl ether) , perfluoro (methylvinyl ether) , hexafluoropropene and tetrafluoroethylene were obtained from DuPont Fluoroproducts (Wilmington, DE) .
  • 1-Butyl-methylimidazolium chloride was obtained from Fluka (Sigma-Aldrich, St. Louis, MO) .
  • Tetra-n- butylphosphonium bromide and tetradecyl (tri-n- hexyl) phosphonium chloride were obtained from Cytec (Canada Inc., Niagara Falls, Ontario, Canada) .
  • 1,1,2,2- Tetrafluoro-2- (pentafluoroethoxy) sulfonate was obtained from SynQuest Laboratories, Inc. (Alachua, FL) .
  • a 1-gallon Hastelloy® C276 reaction vessel was charged with a solution of potassium sulfite hydrate (176 g, 1.0 mol) , potassium metabisulfite (610 g, 2.8 mol) and deionized water (2000 ml) .
  • the pH of this solution was 5.8.
  • the vessel was cooled to 18 degrees C, evacuated to 0.10 MPa, and purged with nitrogen. The evacuate/purge cycle was repeated two more times.
  • To the vessel was then added tetrafluoroethylene (TFE, 66 g) , and it was heated to 100 degrees C at which time the inside pressure was 1.14 MPa.
  • the reaction temperature was increased to 125 degrees C and kept there for 3 hr .
  • TFE pressure decreased due to the reaction
  • more TFE was added in small aliquots (20- 30 g each) to maintain operating pressure roughly between 1.14 and 1.48 MPa.
  • 500 g (5.0 mol) of TFE had been fed after the initial 66 g precharge, the vessel was vented and cooled to 25 degrees C.
  • the pH of the clear light yellow reaction solution was 10-11. This solution was buffered to pH 7 through the addition of potassium metabisulfite (16 g) .
  • the water was removed in vacuo on a rotary evaporator to produce a wet solid.
  • the solid was then placed in a freeze dryer (Virtis Freezemobile 35x1; Gardiner, NY) for 72 hr to reduce the water content to approximately 1.5 wt % (1387 g crude material) .
  • the theoretical mass of total solids was 1351 g.
  • the mass balance was very close to ideal and the isolated solid had slightly higher mass due to moisture.
  • This added freeze drying step had the advantage of producing a free-flowing white powder whereas treatment in a vacuum oven resulted in a soapy solid cake that was very difficult to remove and had to be chipped and broken out of the flask.
  • the crude TFES-K can be further purified and isolated by extraction with reagent grade acetone, filtration, and drying.
  • a 1-gallon Hastelloy® C276 reaction vessel was charged with a solution of potassium sulfite hydrate (88 g, 0.56 mol) , potassium metabisulfite (340 g, 1.53 mol) and deionized water (2000 ml) .
  • the vessel was cooled to 7 degrees C, evacuated to 0.05 MPa, and purged with nitrogen. The evacuate/purge cycle was repeated two more times.
  • To the vessel was then added perfluoro (ethylvinyl ether) (PEVE, 600 g, 2.78 mol), and it was heated to 125 degrees C at which time the inside pressure was 2.31 MPa.
  • the reaction temperature was maintained at 125 degrees C for 10 hr .
  • the pressure dropped to 0.26 MPa at which point the vessel was vented and cooled to 25 degrees C.
  • the 19 F NMR spectrum of the white solid showed pure desired product, while the spectrum of the aqueous layer showed a small but detectable amount of a fluorinated impurity.
  • the desired isomer is less soluble in water so it precipitated in isomerically pure form.
  • the product slurry was suction filtered through a fritted glass funnel, and the wet cake was dried in a vacuum oven (60 degrees C, 0.01 MPa) for 48 hr .
  • the product was obtained as off-white crystals (904 g, 97% yield) .
  • 19 F NMR (D 2 O) ⁇ -86.5 (s, 3F); -89.2, -91.3 (subsplit ABq, J FF 147 Hz, 2F) ;
  • TGA (N 2 ) : 10% wt . loss @ 362 degrees C, 50% wt . loss @ 374 degrees C.
  • a 1-gallon Hastelloy® C276 reaction vessel was charged with a solution of potassium sulfite hydrate (114 g, 0.72 mol), potassium metabisulfite (440 g, 1.98 mol) and deionized water (2000 ml) .
  • the pH of this solution was 5.8.
  • the vessel was cooled to -35 degrees C, evacuated to 0.08 MPa, and purged with nitrogen. The evacuate/purge cycle was repeated two more times.
  • To the vessel was then added perfluoro (methylvinyl ether) (PMVE, 600 g, 3.61 mol) and it was heated to 125 degrees C at which time the inside pressure was 3.29 MPa.
  • the reaction temperature was maintained at 125 degrees C for 6 hr .
  • TGA (air) 10% wt . loss @ 343 degrees C, 50% wt . loss @ 358 degrees C.
  • TGA (N 2 ) 10% wt . loss @ 341 degrees C, 50% wt . loss @ 357 degrees C.
  • a 1-gallon Hastelloy® C reaction vessel was charged with a solution of anhydrous sodium sulfite (25 g, 0.20 mol) , sodium bisulfite 73 g, (0.70 mol) and of deionized water (400 ml) .
  • the pH of this solution was 5.7.
  • the vessel was cooled to 4 degrees C, evacuated to 0.08 MPa, and then charged with hexafluoropropene (HFP, 120 g, 0.8 mol, 0.43 MPa) .
  • the vessel was heated with agitation to 120 degrees C and kept there for 3 hr .
  • the pressure rose to a maximum of 1.83 MPa and then dropped down to 0.27 MPa within 30 minutes.
  • the vessel was cooled and the remaining HFP was vented, and the reactor was purged with nitrogen.
  • the final solution had a pH of 7.3.
  • the water was removed in vacuo on a rotary evaporator to produce a wet solid.
  • the solid was then placed in a vacuum oven (0.02 MPa, 140 degrees C, 48 hr) to produce 219 g of white solid which contained approximately 1 wt % water.
  • the theoretical mass of total solids was 217 g.
  • the crude HFPS-Na can be further purified and isolated by extraction with reagent grade acetone, filtration, and drying.
  • 1,1,2, 2-tetrafluoroethanesulfonate (Cation, imidazolium; Anion, Formula 1)
  • l-Butyl-2, 3-dimethylimidazolium chloride (22.8 g, 0.121 moles) was mixed with reagent-grade acetone (250 ml) in a large round-bottomed flask and stirred vigorously.
  • TFES-K Potassium 1,1,2,2- tetrafluoroethanesulfonate
  • the reaction mixture was filtered once through a celite/acetone pad and again through a fritted glass funnel to remove the KCl.
  • the acetone was removed in vacuo first on a rotovap and then on a high vacuum line
  • HFPS- K potassium 1, 1, 2, 3, 3, 3-hexafluoropropanesulfonate
  • reagent grade acetone 300 ml
  • the reaction mixture was filtered once through a celite/acetone pad and again through a fritted glass funnel.
  • the acetone was removed in vacuo first on a rotovap and then on a high vacuum line (4 Pa, 25 degrees C) for 2 hr .
  • the product was a viscious light yellow oil (103.8 g, 89% yield) .
  • TFES-K Potassium 1,1,2,2- tetrafluoroethane sulfonate
  • TFES-K Potassium 1,1,2,2- tetrafluoroethanesulfonate
  • TGA (N 2 ) : 10% wt . loss @ 375 degrees C, 50% wt . loss @ 410 degrees C.
  • TFES-K Potassium 1,1,2,2- tetrafluoroethanesulfonate
  • TFE Tetrafluoroethylene
  • TTES l-Butyl-3-methylimidazolium chloride
  • deionized water 15 ml
  • TTES-K 16.4 g
  • deionized water 90 ml
  • deionized water 90 ml
  • the layers were separated, and the aqueous phase was extracted with 2 x 50 ml portions of methylene chloride.
  • the combined organic layers were dried over magnesium sulfate and concentrated in vacuo.
  • the colorless oil product was dried at for 4 hr at 5 Pa and 25 degrees C to afford 15.0 g of product.
  • TPES l-Butyl-3-methylimidazolium chloride
  • dry acetone 150 ml
  • potassium 1, 1, 2-trifluoro-2- (perfluoroethoxy) ethanesulfonate TPES-K, 15.0 g
  • TPES-K potassium 1, 1, 2-trifluoro-2- (perfluoroethoxy) ethanesulfonate
  • the reaction mixture was filtered once through a celite/acetone pad and again through a fritted glass funnel to remove the KCl.
  • the acetone was removed in vacuo first on a rotovap and then on a high vacuum line (4 Pa, 25 degrees C) for 2 hr . Residual KCl was still precipitating out of the solution, so methylene chloride (50 ml) was added to the crude product which was then washed with deionized water (2 x 50 ml) .
  • the solution was dried over magnesium sulfate, and the solvent was removed in vacuo to give the product as a viscous light yellow oil (12.0 g, 62% yield) .
  • the oil slowly solidified (439 g) and was removed by suction filtration and then dissolved in chloroform (300 ml) .
  • the chloroform layers were combined and washed with an aqueous sodium carbonate solution (50 ml) to remove any acidic impurity. They were then dried over magnesium sulfate, suction filtered, and reduced in vacuo first on a rotovap and then on a high vacuum line (4 Pa, 100 degrees C) for 16 hr to yield the final product as a white solid (380 g, 76% yield) .
  • TPES-K perfluoroethoxy ethanesulfonate
  • TGA (N 2 ) : 10% wt . loss @ 315 degrees C, 50% wt . loss @ 343 degrees C.
  • TTES-K (trifluoromethoxy) ethanesulfonate
  • the precipitate was removed by suction filtration, and the acetone was removed in vacuo on a rotovap to produce the crude product as a cloudy oil.
  • the product was diluted with ethyl ether (100 ml) and then washed once with deionized water (50 ml), twice with an aqueous sodium carbonate solution (50 ml) to remove any acidic impurity, and twice more with deionized water
  • TGA (N 2 ) : 10% wt . loss @ 328 degrees C, 50% wt . loss @ 360 degrees C.
  • TPENTAS 1- ethyl-3-methylimidazolium chloride (Emim-Cl, 98%, 18.0 g) and reagent grade acetone (150 ml) . The mixture was gently warmed (50 degrees C) until all of the Emim-Cl dissolved.
  • potassium 1,1,2, 2-tetrafluoro-2- (pentafluoroethoxy) sulfonate (TPENTAS-K, 43.7 g) was dissolved in reagent grade acetone (450 ml) .
  • KCl white precipitate
  • the mixture was stirred at 24 degrees C for 8 hr .
  • the KCl precipitate was then allowed to settle leaving a clear yellow solution above it.
  • the KCl was removed by filtration through a celite/acetone pad.
  • the acetone was removed in vacuo to give a yellow oil which was then diluted with chloroform (100 ml) .
  • the chloroform was washed three times with deionized water (50 ml) , dried over magnesium sulfate, filtered, and reduced in vacuo first on a rotovap and then on a high vacuum line (4 Pa, 25 degrees C) for 8 hr .
  • the product was a light yellow oil (22.5 g) .
  • TPES-K perfluoroethoxy ethanesulfonate
  • Trioctyl phosphine 31 g was partially dissolved in reagent-grade acetonitrile (250 ml) in a large round-bottomed flask and stirred vigorously. 1,1,1,2,2,3,3,4,4,5,5,6, 6-Tridecafluoro-8-iodooctane (44.2 g) was added, and the mixture was heated under reflux at 110 degrees C for 24 hours. The solvent was removed under vacuum giving (3,3,4,4,5,5,6,6,7,7,8,8,8- tridecafluorooctyl) -trioctylphosphonium iodide as a waxy solid (30.5 g) .
  • TFES-K Potassium 1,1,2,2- tetrafluoroethanesulfonate
  • reagent grade acetone 100 ml
  • 3, 3, 4, 4, 5, 5, 6, 6, 7, 7, 8, 8, 8 -tridecafluorooctyl 3, 3, 4, 4, 5, 5, 6, 6, 7, 7, 8, 8, 8 -tridecafluorooctyl
  • trioctylphosphonium iodide 60 g
  • the reaction mixture was heated at 60 degrees C under reflux for approximately 16 hours.
  • the reaction mixture was then filtered using a large frit glass funnel to remove the white KI precipitate formed, and the filtrate was placed on a rotary evaporator for 4 hours to remove the acetone.
  • 1,1,1,2,2,3,3,4,4,5,5,6, 6-Tridecafluoro-8-iodooctane (26 g, 0.053 mol) was added, and the mixture was heated under reflux at 110 degrees C for 24 hours. The solvent was removed under vacuum giving l-methyl-3- (3,3,4,4,5,5,6,6,7,7,8,8,8- tridecafluorooctyl) imidazolium iodide (30.5 g) as a waxy solid.
  • TFES-K Potassium 1,1,2,2- tetrafluoroethanesulfonate
  • reaction mixture was then filtered using a large frit glass funnel to remove the white KI precipitate formed, and the filtrate was placed on a rotary evaporator for 4 hours to remove the acetone.
  • the oily liquid was then filtered a second time to yield the product, as shown by proton NMR.
  • Examples 1-2 illustrate the formation of dibutyl ether from 1-butanol.
  • Example 1 Conversion of n-butanol to dibutyl ether 1-Butanol (30 g) , l-ethyl-3-methylimidazolium 1, 1, 2, 2-tetrafluoroethanesulfonate (5 g) , and 1,1,2,2- tetrafluoroethanesulfonic acid (0.6 g) were placed in a 200 ml shaker tube. The tube was heated under pressure with shaking for 6 h at 180 0 C. The vessel was then cooled to room temperature, and the pressure was released.
  • the top phase was shown by proton NMR to contain greater than 75% dibutyl ether with less than 25% 1- butanol, and did not contain measurable quantities of ionic liquid or catalyst.
  • the bottom phase was shown to contain 1, 1, 2, 2-tetrafluoroethanesulfonic acid, 1- ethyl-3-methylimidazolium 1,1,2,2- tetrafluoroethanesulfonate, water and about 10% 1- butanol by weight relative to the combined weight of the ionic liquid, acid catalyst, water and butanol.
  • the conversion of 1-butanol was estimated to be about 90%.
  • the two liquid phases were very distinct and separated within several minutes ( ⁇ 5 min) .

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Catalysts (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

Procédés de fabrication de dialkyl éthers à partir d'alcools à caîne droite en C4-C8 au moyen d'un liquide ionique^.
PCT/US2008/075302 2007-09-05 2008-09-05 Procédés de fabrication de dialkyl éthers à partir d'alcools WO2009032959A2 (fr)

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EP08829069A EP2185495A2 (fr) 2007-09-05 2008-09-05 Procédés de fabrication de dialkyl éthers à partir d'alcools
JP2010524155A JP2010538082A (ja) 2007-09-05 2008-09-05 アルコールからジアルキルエーテルを形成する方法
US12/676,160 US20100197974A1 (en) 2007-09-05 2008-09-05 Processes for making dialkyl ethers from alcohols
CN200880105427.0A CN101796010A (zh) 2007-09-05 2008-09-05 由醇来制备二烷基醚的方法

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CN105017143A (zh) * 2015-07-21 2015-11-04 中国科学院上海有机化学研究所 N-三氟甲氧基吡啶盐类化合物及其制备方法和用途
US10105644B2 (en) 2016-06-14 2018-10-23 Evonik Degussa Gmbh Process and absorbent for dehumidifying moist gas mixtures
US10138209B2 (en) 2016-06-14 2018-11-27 Evonik Degussa Gmbh Process for purifying an ionic liquid
US10493400B2 (en) 2016-06-14 2019-12-03 Evonik Degussa Gmbh Process for dehumidifying moist gas mixtures
US10500540B2 (en) 2015-07-08 2019-12-10 Evonik Degussa Gmbh Method for dehumidifying humid gas mixtures using ionic liquids
US10512883B2 (en) 2016-06-14 2019-12-24 Evonik Degussa Gmbh Process for dehumidifying moist gas mixtures
US10512881B2 (en) 2016-06-14 2019-12-24 Evonik Degussa Gmbh Process for dehumidifying moist gas mixtures

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CN104628538A (zh) * 2013-11-07 2015-05-20 范月辉 一种二丁醚的合成方法
CA3121202A1 (fr) 2018-11-30 2020-06-04 Nuvation Bio Inc. Composes pyrrole et pyrazole et leurs procedes d'utilisation

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US2844534A (en) * 1952-10-20 1958-07-22 Exxon Research Engineering Co High molecular weight branched-chain ethers of lubricating grade
US3267156A (en) * 1961-08-07 1966-08-16 Socony Mobil Oil Co Inc Production of dialkyl ethers
CN100494203C (zh) * 2002-04-05 2009-06-03 南阿拉巴马大学 功能化的离子液体及其使用方法
JP2009502894A (ja) * 2005-07-27 2009-01-29 ビーピー ピー・エル・シー・ 脱水方法
DE102005036457A1 (de) * 2005-08-03 2007-02-08 Merck Patent Gmbh Dehydratisierung von Alkoholen zu Alkenen

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US10500540B2 (en) 2015-07-08 2019-12-10 Evonik Degussa Gmbh Method for dehumidifying humid gas mixtures using ionic liquids
CN105017143A (zh) * 2015-07-21 2015-11-04 中国科学院上海有机化学研究所 N-三氟甲氧基吡啶盐类化合物及其制备方法和用途
CN105017143B (zh) * 2015-07-21 2018-06-26 中国科学院上海有机化学研究所 N-三氟甲氧基吡啶盐类化合物及其制备方法和用途
US10105644B2 (en) 2016-06-14 2018-10-23 Evonik Degussa Gmbh Process and absorbent for dehumidifying moist gas mixtures
US10138209B2 (en) 2016-06-14 2018-11-27 Evonik Degussa Gmbh Process for purifying an ionic liquid
US10493400B2 (en) 2016-06-14 2019-12-03 Evonik Degussa Gmbh Process for dehumidifying moist gas mixtures
US10512883B2 (en) 2016-06-14 2019-12-24 Evonik Degussa Gmbh Process for dehumidifying moist gas mixtures
US10512881B2 (en) 2016-06-14 2019-12-24 Evonik Degussa Gmbh Process for dehumidifying moist gas mixtures

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CN101796010A (zh) 2010-08-04
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